Negative electrode can, alkaline cell and production method for same
The invention provides a mercury-free alkaline cell which does not generate a hydrogen gas. The alkaline cell according to the invention contains a positive electrode, a negative electrode comprising zinc alloy powder, a separator which separates the positive electrode from the negative electrode, an alkaline electrolyte, a positive electrode can imparted with the positive electrode, a negative electrode can imparted with the negative electrode which has a tin-coated layer formed after subjected to a surface treatment with an electrically conductive polymer and comes in contact with the negative electrode via the tin-coated layer and a gasket interposed between the positive electrode can and the negative electrode can.
1. Field of the Invention
The present invention relates to a coin-type alkaline cell or a button-type alkaline cell.
2. Related Art
An alkaline cell used for a small-sized electronic appliance such as a wrist watch is, as shown in
The negative electrode can 4 is press-formed in a cup shape from a triple-layered cladding material having a nickel layer 7 made of nickel, a stainless steel layer 8 made of stainless steel and a current collector layer 9 made of copper.
The positive electrode can 2 holds a positive electrode 1, while the negative electrode can 4 holds a negative electrode 3 which contains mercury-free zinc or zinc alloy powder as a negative electrode active material. The negative electrode 3 is separated from the positive electrode 1 by a separator 5 and is filled with an alkaline electrolyte.
The negative electrode 3 is allowed to use amalgamated zinc pin place of zinc or zinc alloy powder, to thereby suppress generation of a hydrogen gas (H2) from zinc or zinc alloy powder or suppress the generation of the hydrogen gas (H2) from the current collector layer 9 in which the hydrogen gas is ordinarily generated by allowing zinc or zinc alloy powder to come into contact with copper thereof of the negative electrode can through the alkaline electrolyte. The generation of the hydrogen gas results from a reaction which dissolves zinc or zinc alloy powder in the alkaline electrolyte, while oxidizing zinc into zinc oxide. The generation of the hydrogen gas is suppressed, as described above, by using the amalgamated zinc. The consequence is the avoidance of capacity deterioration due to hydrogen generation and leakage and swelling of the cell due to an increased internal pressure.
Recently, there is a trend toward avoiding the use of mercury in coin-type or button-type alkaline cells as far as possible from the environmental point of view, and many researches are being made for this purpose.
SUMMARY OF THE INVENTIONAn alkaline cell according to the present invention contains a positive electrode, a negative electrode having zinc alloy powder, a separator which separates the positive electrode from the negative electrode, an alkaline electrolyte, a positive electrode can imparted with the positive electrode, a negative electrode can imparted with the negative electrode and a gasket interposed between the positive electrode can and the negative electrode can, in which the negative electrode can has a tin-coated layer formed after subjected to a surface treatment with an electrically conductive polymer and comes in contact with the negative electrode via the tin-coated layer.
The negative electrode can according to the invention contains a tin-coated layer formed after subjected to a surface treatment with polyaniline.
Further, a method for producing an alkaline cell according to the invention contains a first step of subjecting a negative electrode can to a surface treatment with polyaniline, a second step of forming a tin-coated layer on the negative electrode can, a third step of subjecting the tin-coated layer to a thermal treatment at a melting point of tin (232° C.) or higher, and a fourth step of folding back a positive electrode can and a negative electrode can which contain a positive electrode, a negative electrode, a separator and an alkaline electrolyte such that a gasket is interposed therebetween and, then, tightening such folded portion for a hermetic sealing.
A method for producing a negative electrode can for use in an alkaline cell according to the invention contains a fist step of subjecting a negative electrode can to a surface treatment with polyaniline, and a second step of forming a tin-coated layer on the negative electrode can.
Further, an alkaline cell according to the invention contains a positive electrode, a negative electrode containing zinc alloy powder, a separator which separates the positive electrode from the negative electrode, an alkaline electrolyte, a positive electrode can imparted with the positive electrode, a negative electrode can imparted with the negative electrode and a gasket interposed between the positive electrode can and the negative electrode can, in which the negative electrode can has a current collector layer containing copper, a tin-coated layer formed on the current collector layer after a surface thereof is subjected to an ionization treatment such that the surface has a cuprous ion and comes in contact with the negative electrode via the tin-coated layer.
A method for producing an alkaline cell according to the invention contains a fist step of subjecting a surface of a current collector layer of a negative electrode can having the current collector layer containing copper to an ionization treatment such that the surface has a cuprous ion, a second step of forming a tin-coated layer on the negative electrode can, a third step of subjecting the tin-coated layer to a thermal treatment at a melting point of thin or higher, and a fourth step of folding back a positive electrode can and a negative electrode can which contain a positive electrode, a negative electrode, a separator and an alkaline electrolyte such that a gasket is interposed therebetween and, then, tightening such folded portion for a hermetic sealing.
In order to effectively suppress the generation of the hydrogen gas, a method for applying a coating layer containing tin which is a metal having a higher hydrogen overpotential than copper is desirable.
According to the invention, hydrogen gas (H2) which will be generated by allowing zinc which is a negative electrode active material to come into contact with the current collector (copper) layer of the negative electrode can is suppressed, corrosion of zinc is suppressed and, then, a leak resistance property against a creeping-up phenomenon of the alkaline electrolyte can be enhanced.
It is possible to form a tin-coated layer having no defect such as a pinhole or a crack and having a uniform thickness when the negative electrode can is subjected to a surface treatment with an electrically conductive polymer such as polyaniline before the tin-coated layer is formed on the negative electrode can. When a surface of a copper layer (current collector layer) of the negative electrode can is treated with the electrically conductive polymer, a surface thereof comes to be composed of Cu+ alone (monovalent copper ion), to thereby form the tin-coated layer having no defect and having a uniform thickness. However, unless the surface of the copper layer (current collector layer) of the negative electrode can is treated, Cu+ and Cu2+ are present in a random manner, to thereby interfere with formation of a uniform tin-coated layer.
Further, according to the invention, since an outer peripheral portion 6b of a projected portion 6a of the gasket at the center side is allowed to come in contact with an inner face of the negative electrode can 4, a leakage resistance property is enhanced and, even when a certain extent of variation of accuracy is present at the time the tin-coated film is provided on an inner face of the negative electrode can, transfer of the alkaline electrolyte is prevented by the fact that the outer peripheral portion 6b of the projected portion of the gasket at the center side is in contact with the inner face of the negative electrode can and, further, since a space between the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side and an inner face of the negative electrode can 4 is 0.05 mm or less, the transfer of zinc powder in the negative electrode is prevented and, further, different from a case in which a tip end of the gasket comes in contact with the inner face of the negative electrode can, since the projected portion of the gasket at the center side does not serve as a support of the negative electrode can at the time of sealing the cell and, then, contact between the negative electrode and the positive electrode in the cell is not interfered and corrosion reaction of zinc which is a negative electrode active material of the current collector (copper) layer of the negative electrode can is not progressed, to thereby improve the deterioration of a capacity retention property.
According to the invention, the alkaline cell which is excellent in a discharge property can be realized without using mercury.
BRIEF DESCRIPTION OF THE DRAWINGS
The alkaline cell of the present invention is now described in detail with reference to preferred embodiments shown in
The positive electrode can 2 is made of a stainless steel sheet with nickel plating. It functions also as a positive electrode terminal. The positive electrode can 2 holds the positive electrode 1 formed in a coin-like or button-like pellet. Then, a separator 5 is arranged on the positive electrode 1 held in the positive electrode can 2. The separator 5 may be a triple-layer laminate composed of a non-woven fabric, cellophane and a sheet of graft-polymerized polyethylene. The separator 5 is impregnated with an alkaline electrolyte. The alkaline electrolyte can be an aqueous solution of sodium hydroxide or potassium hydroxide, or a mixed aqueous solution of sodium hydroxide and potassium hydroxide.
The ring gasket 6 is arranged on an inner peripheral face of the open end edge of the positive electrode can 2. Then, the negative electrode 3 is placed on the separator 5. The negative electrode 3 is a gel-like substance composed of a mercury-free zinc or zinc alloy powder, an alkaline electrolyte and a thickener.
The negative electrode can 4 is inserted into the open end edge of the positive electrode can 2 such that the negative electrode 3 is contained. In the negative electrode can 4, a folded portion 4a in which an open edge end thereof is folded back along an outer peripheral face in a U-shape as cross-section and a folded bottom portion 4b are formed. At the folded portion 4a, the negative electrode can 4 is tightened with an inner peripheral face of the open end edge of the positive electrode can 2 via the gasket 6, to thereby achieve hermetical sealing.
The negative electrode can 4 is press-formed in a cup shape from a triple-layered cladding material composed of a nickel layer 7, a stainless steel layer 8, and a current collector layer 9 made of copper, with the current collector layer 9 being inside and, then, subjected to a surface treatment with an electrically conductive polymeric material such as polyaniline and, thereafter, subjected to, for example, electroless plating of tin, to thereby form a tin-coated layer 10 thereon (
Further, when the tin-coated layer is provided only in an inner face region 11 of the negative electrode can, the leakage resistance property is enhanced, which is preferred. The term “inner face region” as used herein is defined as an inside (side to be in contact with electrolyte) of the negative electrode can 4 as well as an region of a face more inner than the folded bottom portion 4b. The tin-coated layer is not formed in the folded portion 4a which is in contact with the gasket and the folded bottom portion 4b and prevents the electrolyte from creeping up by a creeping phenomenon, to thereby enhance the leakage resistance property. This is because the alkaline electrolyte more likely crept up on the tin-coated layer 10 rather than the current collector layer 9.
By covering unnecessary portions (the folded portion 4a which has been folded back along the outer peripheral face in a U-shape as cross-section and the folded bottom portion 4b) with a masking tape or the like, only the inner face region of the negative electrode can is subjected to a surface treatment with the electrically conductive polymeric material such as polyaniline and, then, the tin-coated layer can be formed thereon by the electroless plating of tin.
In other case, the triple-layered cladding material described above is press-formed in a cup shape with the current collector layer 9 being inside, an entire region of a cup copper face is subjected to a surface treatment with the electrically conductive polymer such as polyaniline, the tin-coated layer is formed with electroless plating and, then, by removing or peeling the unnecessary portions by means of etching using an acid or the like, the tin-coated layer can be formed only on the inner face region of the cup.
When the tin-coated layer is subjected to a thermal treatment, after it is formed, at a temperature of 232° C. which is a melting point of tin or higher, pinholes or cracks which may present in the tin-coated layer can be buried, which is more preferred.
It is preferable that thickness of the tin-coated layer 10 is allowed to be from 0.05 μm to 5 μm. This is because that, in a case in which the thickness is less than 0.05 μm, even when the surface treatment is performed with an electrically conductive polymer, the tin-coated layer having a uniform thickness can not be formed causing defects such as pinholes or cracks, while, in a case in which the thickness is more than 5 μm, the coated layer is liable to be peeled off and, also, it takes a long time to form the coated layer; therefore, none of the above-described cases are preferred.
As for a thermal treatment atmosphere of the tin-coated layer 10, an oxygen concentration is preferably from 0.01% to 1%. For a thermal treatment atmosphere of the tin-coated layer of negative electrode can, it is considered that, by allowing the oxygen concentration to be low as the atmosphere, a surface oxidation of the tin-coated layer can be suppressed. In an atmosphere having an oxygen concentration of over 1%, at the time of subjecting the tin-coated layer 10 to a thermal treatment, there is a risk of causing a problem in a discharge property due to an increase of contact resistance to be derived from oxidation of a tin surface. Further, when the oxygen concentration is lower than 0.01%, a noticeable influence is hardly given to the tin-coated layer 10 and no particular merit is generated at such a low level of the oxygen concentration as described above.
As for the alkaline electrolyte, it is preferable that sodium hydroxide is in the range of from 15 to 30% by weight or potassium hydroxide is in the range of from 1 to 15% by weight. Since an aqueous solution of potassium hydroxide is excellent in electric conductivity compared with an aqueous solution of sodium hydroxide, the aqueous solution of potassium hydroxide is excellent in the electric conductivity even in a small amount. When a ratio of potassium hydroxide in the alkaline electrolyte is less than 1% by weight, enhancement of the discharge property to be caused by the excellent conductivity of the aqueous solution of potassium hydroxide compared with the aqueous solution of sodium hydroxide is small, which is not preferred. Further, when a ratio of potassium hydroxide is more than 15% by weight, since the aqueous solution of potassium hydroxide has a higher wetting property to copper than the aqueous solution of sodium hydroxide, the leakage resistance property of the cell is deteriorated, which is not preferred. Sodium hydroxide and potassium hydroxide can be used as an electrolyte either each individually or in mixture.
Further, by allowing the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side to come to be in contact with the inner face of the negative electrode can 4 or by allowing a space between the outer periphery 6b of the projected portion 6a of the gasket 6 at the center side and the inner face of the negative electrode can 4 to be 0.05 mm or less, the outer peripheral portion 6b of the projected portion 6a of the gasket at the center side does not become a support against the negative electrode can 3 and, then, the contact between the negative electrode and the positive electrode in the cell is not interfered with each other, which is preferred.
As for the positive electrode active materials to be used in the invention, silver oxide, manganese dioxide, a composite oxide of nickel and silver, nickel oxyhydroxide can be used; however the invention is not limited thereto.
EXAMPLE 1 A cell having a constitution as shown in
On the other hand, an alkaline electrolyte containing 22% by weight of sodium hydroxide and 9% by weight of potassium hydroxide was poured into the positive electrode can 2 and, then, a disk-like pellet of the positive electrode 1 was inserted thereinto, to thereby allow the positive electrode 1 to absorb the alkaline electrolyte. Next, the separator 5 which had been pressed off in a circular shape from a triple-layered structure composed of a non-woven fabric, cellophane and a film of graft-polymerized polyethylene was placed on the pellet of the positive electrode 1. Then, the separator 5 was impregnated with an alkaline electrolyte containing 22% by weight of sodium hydroxide and 9% by weight of potassium hydroxide which was added dropwise.
Next, a gel-like negative electrode 3 composed of a mercury-free zinc alloy powder containing aluminum, indium and bismuth, zinc oxide, a thickener, sodium hydroxide, potassium hydroxide and water was placed on the separator 5. The negative electrode can 4 was inserted into the open end edge of the positive electrode can 2 such that it covered the negative electrode 3, with the ring gasket 6 made of nylon-66 and coated with asphalt plus epoxy-type sealant interposed between them. The opening was hermetically sealed by means of caulking. In this way the desired alkaline cell was obtained. In this occasion, the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side was allowed to come into contact with the inner face of the negative electrode can 4.
EXAMPLE 2In the Example 2, a space between the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side and the inner face of the negative electrode can was allowed to be 0.05 mm. Other conditions were same as in Example 1 to prepare the alkaline cell.
EXAMPLE 3In the Example 3, a space between the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side and the inner face of the negative electrode can was allowed to be 0.07 mm. Other conditions were same as in Example 1 to prepare the alkaline cell.
EXAMPLE 4In the Example 4, the alkaline electrolyte was allowed to be a mixed solution containing 15% by weight of sodium hydroxide and 15% by weight of potassium hydroxide. Other conditions were same as in Example 1 to prepare the alkaline cell.
EXAMPLE 5In the Example 5, the alkaline electrolyte was allowed to be a mixed solution containing 30% by weight of sodium hydroxide and 1% by weight of potassium hydroxide. Other conditions were same as in Example 1 to prepare the alkaline cell.
EXAMPLE 6In the Example 6, the alkaline electrolyte was allowed to be a mixed solution containing 30% by weight of sodium hydroxide and 15% by weight of potassium hydroxide. Other conditions were same as in Example 1 to prepare the alkaline cell.
EXAMPLE 7In the Example 7, the alkaline electrolyte was allowed to be a mixed solution containing 30% by weight of sodium hydroxide and 0.5% by weight of potassium hydroxide. Other conditions were same as in Example 1 to prepare the alkaline cell.
EXAMPLE 8In the Example 8, the alkaline electrolyte was allowed to be a mixed solution containing 15% by weight of sodium hydroxide and 20% by weight of potassium hydroxide. Other conditions were same as in Example 1 to prepare the alkaline cell.
COMPARATIVE EXAMPLE 1In Comparative Example 1, an alkaline cell was prepared by using the negative electrode can in which the tin-coated layer having a thickness of 0.1 μm was formed by ordinary electroless plating on the negative electrode can 4. A surface treatment by using polyaniline was not performed on the negative electrode can. Other conditions were same as in Example 1.
210 cells each of Examples 1 to 8 and Comparative Example 1 were prepared. 100 cells out of cells thus prepared in each of Examples 1 to 8 and Comparative Example 1 were stored under a severe environment of 40° C. 90% RH and evaluation results on ratio of occurrence of leakage after 120 days of storage and 140 days of storage are shown in Table 1. Further, 100 cells out of cells thus prepared in each of Examples 1 to 8 and Comparative Example 1 were stored for 100 days under an environment of 60° C. 0% RH and evaluation results on discharge capacity [mAh] at a terminal voltage of 1.2V after 30 kΩ constant discharge are shown in Table 1. Incidentally, in each cell, initial discharge capacity was about 28 mAh. Lastly, 10 cells out of cells thus prepared in each of Examples 1 to 8 and Comparative Example 1 were evaluated on closed circuit voltage [V] after 5 seconds under conditions of initial (depth of discharge: 0%), load resistance: 2 kΩ in an environment of −10° C. The results are shown in Table 1.
Firstly, when Example 1 and Comparative Example 1 are compared with each other on the basis of Table 1, it is found that, by forming the tin-coated layer by using the electroless plating after subjected the negative electrode can to a treatment by an electrically conductive polymeric material such as polyaniline, the leakage resistance property and the capacity retention property can be enhanced. In Example 1, there was no leakage at all both after 120 days and 140 days. To contrast, in Comparative Example 1, 3% showed leakage after 120 days while 10% showed leakage after 140 days. This was because that, in Example 1, by subjecting a plating face to a surface treatment with an electrically conductive polymeric material such as polyaniline before the electroless plating was performed by using tin, dense tin-coated layer free of cracks or pinholes was formed. To contrast, in Comparative Example 1, the negative electrode can was not subjected to a surface treatment by the electrically conductive polymer and there were cracks or pinholes. It was assumed that, since copper which has a lower hydrogen overpotential than tin was exposed, hydrogen was generated and, then, the ratio of occurrence of leakage was increased.
Next, when Examples 1 to 3 were compared thereamong on the basis of Table 1, there was no leakage at all both in Examples 1 and 2. In Example 3, when it was compared with Comparative Example 1, although the ratio of occurrence of leakage thereof was low, about 3% thereof showed leakage after 140 days of storage. In the alkaline cell in which the space between the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side and the inner face of the negative electrode can is 0.05 mm or less, the leakage resistance property and the capacity retention property were excellent. This was because that, by allowing the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side and the inner face of the negative electrode can 4 to come into contact with each other or allowing a space therebetween to be 0.05 mm or less, zinc powder in the negative electrode at the time of sealing the cell was able to be prevented from entering the space between the gasket and the negative electrode can. When zinc powder entered between the gasket and the negative electrode can, zinc powder came into contact with the current collector layer containing copper which has a low hydrogen overpotential, to thereby cause generation of hydrogen gas. Further, a certain extent of error to be generated at the time of assembling the negative electrode can and the gasket or a certain extent of error of a position at which the tin-coated layer is formed can be tolerated so long as the space between the outer peripheral portion 6b of the projected portion 6a of the gasket 6 at the center side and the inner face of the negative electrode can is 0.05 mm or less. Particularly, even when the current collector layer was exposed to some extent due to a variance of an end portion of the tin-coated layer, the zinc powder does not enter the space between the gasket and the negative electrode can and, then, hydrogen is prevented from being generated.
When Examples 4 to 6 were compared thereamong on the basis of Table 1, it is found that, by allowing the alkaline electrolyte to be an aqueous solution in which sodium hydroxide is in an amount of from 15% by weight to 30% by weight and potassium hydroxide is in an amount of from 1 to 15% by weight, a favorable closed circuit voltage property has been obtained. Further, there was no leakage at all in Examples 4 to 6. In order to obtain a favorable closed circuit voltage property, an amount of sodium hydroxide to be added is appropriately in the range of from 15 to 30% by weight.
On the other hand, although Example 7 has no generation of leakage and is more favorable than Example 1, the closed circuit voltage is lower than other Examples. This was because, it is considered, that an amount of potassium hydroxide contained in the alkaline electrolyte was small. The aqueous solution of potassium hydroxide is excellent in conductivity compared with the aqueous solution of sodium hydroxide. For this account, in Example 7 in which the amount of potassium hydroxide to be contained is small, it is considered that the closed circuit voltage has been lowered. For this account, in a case in which the closed circuit voltage was taken into a serious consideration, it is preferable that potassium hydroxide is contained in an amount of 1% by weight or more in the alkaline electrolyte.
In Example 8, leakage was generated after 140 days of storage. This was because an amount of potassium hydroxide contained in the alkaline electrolyte was large. Since the aqueous solution of potassium hydroxide has a higher wetting property to copper than the aqueous solution of sodium hydroxide, when the amount of potassium hydroxide is large, a creep phenomenon is generated, to thereby cause leakage. In order to improve the leakage resistance property, it is particularly preferable that the amount of potassium hydroxide to be contained is allowed to be 15% by weight or less.
Further, as for coating layer for the negative electrode can, not only tin but also at least one metal or alloy of indium (melting point: 156.6° C.) and bismuth (melting point: 271.4° C.) and alloys thereof is permissible as a metal or an alloy which has a higher hydrogen overpotential than copper.
According to the invention, since the tin-coated layer 10 free from defects such as pinholes, cracks and contaminations with impurities can be formed inside the negative electrode can 4, the generation of the hydrogen gas (H2) which is otherwise generated by allowing zinc which is a negative electrode active material to be in contact with the current collector layer 9 of the negative electrode can 4 is suppressed, corrosion of zinc is suppressed and, also, leakage resistance property by the creeping-up phenomenon of the alkaline electrolyte can be obtained. According to the invention, a favorable alkaline cell can be obtained without using mercury.
Further, the invention is not limited to such examples and comparative examples as described above. It goes without saying that various changes, modifications and alterations may be made in the invention without departing from the scope and spirit thereof.
Claims
1. An alkaline cell, comprising: a positive electrode; a negative electrode comprising zinc alloy powder; a separator which separates the positive electrode from the negative electrode; an alkaline electrolyte; a positive electrode can imparted with the positive electrode; a negative electrode can imparted with the negative electrode; and a gasket interposed between the positive electrode can and the negative electrode can, wherein the negative electrode can has a tin-coated layer formed after subjected to a surface treatment with an electrically conductive polymer and comes in contact with the negative electrode via the tin-coated layer.
2. The alkaline cell according to claim 1, wherein the positive electrode comprises silver oxide or manganese dioxide.
3. The alkaline cell according to claim 1, wherein the tin-coated layer is formed in the region of an inner face of the negative electrode can.
4. The alkaline cell according to claim 1, wherein the negative electrode can is a negative electrode can comprising a tin-coated layer formed after subjected to a surface treatment with polyaniline.
5. The alkaline cell according to claim 1, wherein the tin-coated layer is a tin-coated layer formed by electroless plating.
6. The alkaline cell according to claim 1, wherein thickness of the tin-coated layer is from 0.05 μm to 5 μm.
7. The alkaline cell according to claim 1,
- wherein the tin-coated layer is a tin-coated layer subjected to a thermal treatment at a melting point of tin or higher.
8. The alkaline cell according to claim 7, wherein the tin-coated layer is a tin-coated layer subjected to a thermal treatment in an atmosphere of an oxygen concentration of 1% or less.
9. The alkaline cell according to claim 1, where in sodium hydroxide is present in an amount of from 15 to 30% by weight or potassium hydroxide is present in an amount of from 1 to 15% by weight in the alkaline electrolyte.
10. The alkaline cell according to claim 1, wherein a peripheral portion of a projected portion of the gasket at the center side comes in contact with an inner face of the negative electrode can or has a space of 0.05 mm or less apart from the inner face of the negative electrode can.
11. A negative electrode can for use in an alkaline cell comprising a tin-coated layer formed after subjected to a surface treatment with polyaniline.
12. A method for producing an alkaline cell comprising:
- a first step of subjecting a negative electrode can to a surface treatment with polyaniline;
- a second step of forming a tin-coated layer on the negative electrode can;
- a third step of subjecting the tin-coated layer to a thermal treatment at a melting point of tin or higher; and
- a fourth step of folding back a positive electrode can and a negative electrode can which contain a positive electrode, a negative electrode, a separator and an alkaline electrolyte such that a gasket is interposed therebetween and, then, tightening such folded portion for a hermetic sealing.
13. A method for producing a negative electrode can for use in an alkaline cell, comprising:
- a fist step of subjecting a negative electrode can to a surface treatment with polyaniline; and
- a second step of forming a tin-coated layer on the negative electrode can.
14. The method for producing the negative electrode can for use in the alkaline cell according to claim 13, further comprising: after the second step, a third step of subjecting the tin-coated layer to a thermal treatment at a melting point of tin or higher.
15. An alkaline cell, comprising: a positive electrode, a negative electrode containing zinc alloy powder, a separator which separates the positive electrode from the negative electrode, an alkaline electrolyte, a positive electrode can imparted with the positive electrode, a negative electrode can imparted with the negative electrode and a gasket interposed between the positive electrode can and the negative electrode can, wherein the negative electrode can has a current collector layer comprising copper, a tin-coated layer formed on the current collector layer after a surface thereof is subjected to an ionization treatment such that the surface has a cuprous ion and comes in contact with the negative electrode via the tin-coated layer.
16. A method for producing an alkaline cell, comprising:
- a fist step of subjecting a surface of a current collector layer of a negative electrode can having the current collector layer comprising copper to an ionization treatment such that the surface has a cuprous ion;
- a second step of forming a tin-coated layer on the negative electrode can;
- a third step of subjecting the tin-coated layer to a thermal treatment at a melting point of thin or higher; and
- a fourth step of folding back a positive electrode can and a negative electrode can which contain a positive electrode, a negative electrode, a separator and an alkaline electrolyte such that a gasket is interposed therebetween and, then, tightening such folded portion for a hermetic sealing.
17. An alkaline cell, comprising: a positive electrode; a negative electrode comprising zinc alloy powder; a separator which separates the positive electrode from the negative electrode; an alkaline electrolyte; a positive electrode can imparted with the positive electrode; a negative electrode can imparted with the negative electrode which has a tin-coated layer formed after subjected to a surface treatment with an electrically conductive polymer and comes in contact with the negative electrode via the tin-coated layer; and a gasket interposed between the positive electrode can and the negative electrode can.
Type: Application
Filed: Nov 29, 2005
Publication Date: Jun 15, 2006
Inventors: Takeshi Shishido (Miyagi), Iwazou Takahashi (Miyagi), Shunji Watanabe (Miyagi), Tsugio Sakai (Miyagi)
Application Number: 11/288,740
International Classification: H01M 2/02 (20060101); H01M 4/42 (20060101); H01M 4/54 (20060101); H01M 4/50 (20060101); H01M 2/08 (20060101); H01M 10/04 (20060101); H01M 4/66 (20060101);
